CN205419791U - Device is mediated to chemical method active carbon - Google Patents
Device is mediated to chemical method active carbon Download PDFInfo
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- CN205419791U CN205419791U CN201520848523.1U CN201520848523U CN205419791U CN 205419791 U CN205419791 U CN 205419791U CN 201520848523 U CN201520848523 U CN 201520848523U CN 205419791 U CN205419791 U CN 205419791U
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- kneader
- active carbon
- chemical method
- feed bin
- shell
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Abstract
The utility model discloses a device is mediated to chemical method active carbon, including dry saw -dust feed bin (1), fixed quantity feeder (2), kneading machine (3), activate fluid metering tank (4), during kneading machine (3) are sent into via fixed quantity feeder (2) to dry saw -dust in saw -dust feed bin (1), simultaneously the activator in activate fluid metering tank (4) is after the accurate measurement of height level gauge (4 -1), deliver to kneading machine (3) by confession acid pump (5) management way on, spout the saw -dust by nozzle (3 -1), the rotation along with inside and outside spiral shell area (3 -2) mixes and mediates with the activator to get into the dry saw -dust of kneading machine, mediates the material that obtains after a period by kneading machine (3) through pneumatic discharge valve (3 -3) unloading. The utility model discloses mediate efficiently to adopt the closed system of mediating, reduced the pollution of dry farine, improved the operation environment in workshop effectively.
Description
Technical field
This utility model relates to technique and the device that a kind of active carbon by chemical method is mediated, and belongs to technical field of active carbon.
Background technology
Ligneous chemical method powdered activated carbon produces, often use wood flour to be dried, mediate, charcoal activation, pickling, the workshop section such as dry, pulverizing.Wood flour is mediated as the important step produced with activator, directly affects the final performance of product, such as sub-orchid, caramel etc..
Conventional chemical methods powdered activated carbon uses discontinuous slurry mixer, the shortcoming such as this device exists that work efficiency is low, the amount i.e. bad control of solid-liquid ratio of wood flour and activator, being eliminated the most progressively；Some producer began to use successional pair of flood dragon kneader in recent years, this method equally exist wood flour mix with activator uneven, be dried fine powder flying dust and affect the shortcoming such as operating environment in workshop, the most non-large area is generalized use.
Utility model content
This utility model, for the deficiency of the problems referred to above, proposes a kind of active carbon by chemical method kneader and kneader process thereof, and it mediates efficiency height, and uses closed kneading system, reduces the pollution of dry fine powder, effectively improves the operating environment in workshop.
This utility model is that the technical scheme solving the proposition of above-mentioned technical problem is:
A kind of active carbon by chemical method kneader, including dried wood chips feed bin (1), fixed quantity feeder (2), kneader (3), activating solution measuring tank (4)；Described dried wood chips feed bin (1) is arranged on kneader (3), and described fixed quantity feeder (2) is arranged between dried wood chips feed bin (1) and kneader (3)；Described kneader (3) is double ribbon mixers, and described pair of ribbon mixer includes shell, more than one nozzle (3-1), double ribbon (3-2), pneumatic outlet valve (3-3), decelerating through motor power plants (3-4)；Described pair of ribbon (3-2) is arranged in shell, and the two ends of double ribbon (3-2) are rotationally connected with shell by bearing respectively, and described decelerating through motor power plants (3-4) is connected with one end of double ribbons (3-2), described nozzle (3-1) is arranged at the top of shell, and being axially uniformly distributed along double ribbon (3-2)；Described pneumatic outlet valve (3-3) is arranged at the bottom of shell；Described activating solution measuring tank (4) is connected with nozzle (3-1) by pipeline, and described pipeline is disposed with for acid pump (5) and stop valve (6).
Further: also include that automatic control cabinet (7), described fixed quantity feeder (2), decelerating through motor power plants (3-4), pneumatic outlet valve (3-3), confession acid pump (5) and stop valve (6) are all connected with automatic control cabinet (7).
Further: described activating solution measuring tank (4) is provided with two position meter (4-1).
Preferred: in described activating solution measuring tank (4), to be loaded with phosphoric acid or zinc chloride.
A kind of method that active carbon by chemical method is mediated, the dried wood chips in wood flour feed bin (1) is sent in kneader (3) via fixed quantity feeder (2)；Activator in activating solution measuring tank (4) is after two position meter (4-1) measures simultaneously, by delivering on kneader (3) by the road for acid pump (5), nozzle (3-1) is being sprayed onto in wood flour；Enter the dried wood chips of kneader and activator and carry out mixing and mediating along with the rotation of inside and outside ribbon (3-2), the material obtained after mediating a period of time by kneader (3) by pneumatic outlet valve (3-3) emptying.
A kind of active carbon by chemical method kneader of the present utility model and kneader process thereof, compared to existing technology, having the advantages that owing to being provided with dried wood chips feed bin (1), fixed quantity feeder (2), kneader (3), activating solution measuring tank (4), the dried wood chips in wood flour feed bin (1) is sent in kneader (3) via fixed quantity feeder (2)；Activator in activating solution measuring tank (4) is after two position meter (4-1) measures simultaneously, by delivering on kneader (3) by the road for acid pump (5), nozzle (3-1) is being sprayed onto in wood flour；Enter the dried wood chips of kneader and activator and carry out mixing and mediating along with the rotation of inside and outside ribbon (3-2), the material obtained after mediating a period of time is vented by pneumatic outlet valve (3-3) by kneader (3), therefore the major influence factors solid-liquid ratio affecting chemical method production activated carbon is accurately controlled by this utility model, greatly improve kneading efficiency, and use closed kneading system, reduce the pollution of dry fine powder, effectively improve the operating environment in workshop.
Accompanying drawing explanation
Fig. 1 is this utility model one active carbon by chemical method kneader；
Detailed description of the invention
Accompanying drawing discloses the structural representation of one preferred embodiment of this utility model without limitation, explains the technical solution of the utility model below with reference to accompanying drawing.
Embodiment
A kind of active carbon by chemical method kneader of the present embodiment, as it is shown in figure 1, include dried wood chips feed bin (1), fixed quantity feeder (2), kneader (3), activating solution measuring tank (4)；Described dried wood chips feed bin (1) is arranged on kneader (3), and described fixed quantity feeder (2) is arranged between dried wood chips feed bin (1) and kneader (3)；Described kneader (3) is double ribbon mixers, and described pair of ribbon mixer includes shell, more than one nozzle (3-1), double ribbon (3-2), pneumatic outlet valve (3-3), decelerating through motor power plants (3-4)；Described pair of ribbon (3-2) is arranged in shell, and the two ends of double ribbon (3-2) are rotationally connected with shell by bearing respectively, and described decelerating through motor power plants (3-4) is connected with one end of double ribbons (3-2), described nozzle (3-1) is arranged at the top of shell, and being axially uniformly distributed along double ribbon (3-2)；Described pneumatic outlet valve (3-3) is arranged at the bottom of shell；Described activating solution measuring tank (4) is connected with nozzle (3-1) by pipeline, and described pipeline is disposed with for acid pump (5) and stop valve (6).
Also include that automatic control cabinet (7), described fixed quantity feeder (2), decelerating through motor power plants (3-4), pneumatic outlet valve (3-3), confession acid pump (5) and stop valve (6) are all connected with automatic control cabinet (7).
Described activating solution measuring tank (4) is provided with two position meter (4-1).
It is loaded with phosphoric acid or zinc chloride in described activating solution measuring tank (4).
A kind of method that active carbon by chemical method is mediated, the programme-control set by automatic control cabinet (7), the fixed quantity feeder (2) that a certain amount of dried wood chips in wood flour feed bin (1) controlled via the time is sent in kneader (3), activator phosphoric acid in activating solution measuring tank (4) or zinc chloride are after liquidometer (4-1) accurately metering simultaneously, by delivering on kneader (3) by the road for acid pump (5), it is sprayed onto in wood flour by nozzle (3-1), enter the material of kneader and activator and carry out mixing and mediating along with the rotation of inside and outside ribbon (3-2), after mediating a period of time, material is vented by kneader (3) pneumatic outlet valve (3-4), enter lower road charcoal and activate workshop section, one loop ends, sequentially enter next circulation.
The major influence factors solid-liquid ratio affecting chemical method production activated carbon is accurately controlled by this utility model by above structure, greatly improve kneading efficiency, and use closed kneading system, reduce the pollution of dry fine powder, effectively improve the operating environment in workshop.
It is merely to illustrate embodiment of the present utility model above in conjunction with this utility model preferred embodiment described by accompanying drawing; not as to aforementioned utility model purpose and claims content and the restriction of scope; every according to technical spirit of the present utility model to any simple modification made for any of the above embodiments, equivalent variations and modification, the most still belong to this utility model technology and rights protection category.
Claims (4)
1. an active carbon by chemical method kneader, it is characterised in that: include dried wood chips feed bin (1), fixed quantity feeder (2), kneader (3), activating solution measuring tank (4)；Described dried wood chips feed bin (1) is arranged on kneader (3), and described fixed quantity feeder (2) is arranged between dried wood chips feed bin (1) and kneader (3)；Described kneader (3) is double ribbon mixers, and described pair of ribbon mixer includes shell, more than one nozzle (3-1), double ribbon (3-2), pneumatic outlet valve (3-3), decelerating through motor power plants (3-4)；Described pair of ribbon (3-2) is arranged in shell, and the two ends of double ribbon (3-2) are rotationally connected with shell by bearing respectively, and described decelerating through motor power plants (3-4) is connected with one end of double ribbons (3-2), described nozzle (3-1) is arranged at the top of shell, and being axially uniformly distributed along double ribbon (3-2)；Described pneumatic outlet valve (3-3) is arranged at the bottom of shell；Described activating solution measuring tank (4) is connected with nozzle (3-1) by pipeline, and described pipeline is disposed with for acid pump (5) and stop valve (6).
Active carbon by chemical method kneader the most according to claim 1, it is characterized in that: also include that automatic control cabinet (7), described fixed quantity feeder (2), decelerating through motor power plants (3-4), pneumatic outlet valve (3-3), confession acid pump (5) and stop valve (6) are all connected with automatic control cabinet (7).
Active carbon by chemical method kneader the most according to claim 1, it is characterised in that: described activating solution measuring tank (4) is provided with two position meter (4-1).
Active carbon by chemical method kneader the most according to claim 1, it is characterised in that: it is loaded with phosphoric acid or zinc chloride in described activating solution measuring tank (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520848523.1U CN205419791U (en) | 2015-10-29 | 2015-10-29 | Device is mediated to chemical method active carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520848523.1U CN205419791U (en) | 2015-10-29 | 2015-10-29 | Device is mediated to chemical method active carbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205419791U true CN205419791U (en) | 2016-08-03 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520848523.1U Expired - Fee Related CN205419791U (en) | 2015-10-29 | 2015-10-29 | Device is mediated to chemical method active carbon |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205419791U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105271226A (en) * | 2015-10-29 | 2016-01-27 | 徐州天正活性炭厂 | Chemical process active carbon kneading equipment and kneading method of chemical process active carbon kneading equipment |
-
2015
- 2015-10-29 CN CN201520848523.1U patent/CN205419791U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105271226A (en) * | 2015-10-29 | 2016-01-27 | 徐州天正活性炭厂 | Chemical process active carbon kneading equipment and kneading method of chemical process active carbon kneading equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160803 Termination date: 20161029 |